US7947240B2ActiveUtilityA1

System and method of carbon capture and sequestration

Assignee: EXPANSION ENERGY LLCPriority: Oct 8, 2008Filed: Oct 8, 2008Granted: May 24, 2011
Est. expiryOct 8, 2028(~2.2 yrs left)· nominal 20-yr term from priority
Inventors:David Vandor
Y02C20/40B01D 2258/0283B01D 53/1475B01D 53/62B01D 53/1493B01D 2257/504F25J 1/0284F25J 2220/44F25J 2210/70Y10S210/908F25J 2220/02F25J 1/007F25J 2270/16B01D 2257/404F25J 1/0288F25J 1/0072B01D 2251/30F25J 1/0204F25J 2230/30F25J 1/005F25J 1/004F25J 2230/20F25J 1/0015
86
PatentIndex Score
14
Cited by
36
References
20
Claims

Abstract

Systems and methods of capturing and sequestering carbon dioxide, comprising mixing a substantially non-aqueous solvent and an alkali such that the solvent and alkali form a solvent suspension, mixing water and a flue gas containing carbon dioxide with the solvent suspension such that a reaction occurs, the reaction resulting in the formation of a carbonate, water and heat.

Claims

exact text as granted — not AI-modified
1. A method of capturing and sequestering carbon dioxide, comprising:
 mixing a substantially non-aqueous solvent and an alkali such that the solvent and alkali form a solvent suspension; 
 mixing water and a flue gas containing carbon dioxide with the solvent suspension in a reaction vessel such that a reaction occurs, the reaction resulting in the rapid formation of a carbonate, water and heat, the resulting water forming a solution with the solvent, the resulting carbonate being essentially free of organo-metallic products and substantially non-aqueous; 
 the resulting carbonate precipitating out of solution, requiring no further chemical processing steps, falling toward the bottom of the reaction vessel, and accumulating at the bottom of the reaction vessel together with some substantially non-aqueous solvent. 
 
     
     
       2. The method of  claim 1  further comprising the steps of:
 continuously removing a portion of the solution of water and solvent from the reaction vessel; 
 separating the water from the solvent; 
 introducing additional alkali to the separated solvent; 
 re-mixing the separated solvent with the additional alkali such that the solvent and additional alkali form a solvent suspension; 
 providing additional flue gas containing carbon dioxide; and 
 returning a portion of the separated water to the solvent suspension to continue the reaction. 
 
     
     
       3. The method of  claim 2  wherein the precipitated carbonate is mechanically removed from the reaction vessel. 
     
     
       4. The method of  claim 1  wherein the solvent is an alcohol. 
     
     
       5. The method of  claim 4  wherein the alcohol is methanol. 
     
     
       6. The method of  claim 5  wherein the alkali reacts with the methanol to form methoxide. 
     
     
       7. The method of  claim 6  further comprising introducing ash into the solvent, wherein one or more constituents of the ash are alkalis and the ash contains one or more metal oxides including iron oxide. 
     
     
       8. The method of  claim 2  wherein separating the water from the solvent includes chilling the solution of water and solvent in a cryogenic drying vessel such that the water falls substantially to the bottom of the cryogenic drying vessel and the solvent rises substantially to the top of the cryogenic drying vessel. 
     
     
       9. The method of  claim 2  wherein separating the water from the solvent includes the steps of: applying heat to the solution of water and solvent, using a partial vacuum to draw off vaporous solvent from a hot distillation vessel, and condensing the vaporous solvent. 
     
     
       10. The method of  claim 2  wherein carbon dioxide and water react to form carbonic acid. 
     
     
       11. The method of  claim 10  further comprising introducing ash into the solvent, one or more constituents of the ash being alkalis and the ash containing one or more metal oxides including iron oxide, wherein the carbonic acid reacts with the alkalis to substantially neutralize the alkalis. 
     
     
       12. The method of  claim 11  wherein the reaction of carbonic acid and the alkalis results in a non-alkaline stream comprising one or more carbonates, sand and iron oxide. 
     
     
       13. The method of  claim 2  wherein the reaction temperature is less than about 150 degrees Fahrenheit. 
     
     
       14. A method of separating chemical constituents of flue gas, comprising:
 mixing a substantially non-aqueous solvent and an alkali such that the solvent and alkali form a solvent suspension; 
 introducing water and a flue gas containing carbon dioxide and nitrogen to the solvent suspension; 
 contacting the alkali in the solvent suspension with the water and the carbon dioxide in the flue gas in a reaction vessel such that a reaction occurs, the reaction resulting in the rapid formation of a substantially non-aqueous carbonate, water and heat, the carbonate being essentially free of organo-metallic products, and the resulting water forming a solution with the solvent; 
 removing the solution of water and solvent from the reaction vessel such that the resulting carbonate is substantially non-aqueous; and 
 substantially liquefying a portion of the nitrogen by compressing and chilling the nitrogen. 
 
     
     
       15. A method of capturing or sequestering carbon dioxide, comprising:
 mixing methanol and an alkali such that the methanol and alkali form a solvent suspension; 
 mixing water and a flue gas containing carbon dioxide with the solvent suspension such that a reaction occurs, the reaction resulting in the rapid formation of a substantially non-aqueous carbonate, water and heat, the carbonate being essentially free of organo-metallic products. 
 
     
     
       16. The method of  claim 15  wherein the alkali reacts with the methanol to form methoxide. 
     
     
       17. The method of  claim 16  further comprising introducing ash into the solvent, wherein one or more constituents of the ash are alkalis and the ash contains one or more metal oxides including iron oxide. 
     
     
       18. The method of  claim 15  wherein the resulting water forms a solution with the methanol and the resulting carbonate precipitates out of solution, requiring no further chemical processing steps, falls toward the bottom of the reaction vessel, and accumulates at the bottom of the reaction vessel together with some methanol. 
     
     
       19. The method of  claim 18  further comprising the steps of:
 continuously removing a portion of the solution of water and methanol from the reaction vessel such that the resulting carbonate is substantially non-aqueous; 
 separating the water from the solvent; 
 introducing additional alkali to the separated solvent; 
 re-mixing the separated solvent with the additional alkali such that the methanol and additional alkali form a solvent suspension; 
 providing additional flue gas containing carbon dioxide; and 
 returning a portion of the separated water to the solvent suspension to continue the reaction. 
 
     
     
       20. The method of  claim 16  wherein the water content of the methanol does not exceed about 10% by volume.

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